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4. Advection-diffusion on a bounded domain: Suppose that a large population of ants is following a pheromone trail to a new n

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\partialp/\partialt = D\partial2p/\partialx2 - u\partialp/\partialx

a). where D is a constant.  We can write down a general solution describing how it will disperse , but we need to specialise to our specific case to get a physical applicable answer.

Remember the tubes were sealed at both ends ; this means the flow substance at either end of the tube has to be zero. It turns out this is proportional to the first derivative, \partialxc of the concentration. So we would like this to be zero at the both ends.

\partialc/\partialx\midx=0x = 0,  \partialc/\partialx\midx=L = 0.

In this case it is of the form , c(x,0) ~ \delta(x) since we injectb all point. A condition which a quantity that varies throughout a given space or enclosure must fulfill at every point on the boundary of that space especially when the velocity of a fluid at any point on the wall a rigid conduit is necessary parallel to the wall. For example, if the independent variable is time over the domain [0,1], a boundary value problem would specify values fpr y(t) at both t = 0 and t=1 , whereas an initial value problem would specify a vlaue of y(t) and y'(t) at time t = 0.

b). In other words it makes some sense that we should expect that as t\rightarrow\infty our tempratue distribution, u (x,t) should behaves as,

liim u (x,t) = uE (x)

where, uE (x) is called the equilibium temperature. Note as well that is should still satisfy the heat equation and boundary conditons. It would not satisfy the initial condition however because it is the temperature distribution as t \rightarrow\infty whereas the initial condition is at t = 0. So, the eqilibirium temperature distribution should satisfy,

0 = d2uE/dx2 uE (0) = T1 uE (L) = T2

This is a really ordinary differential equation. If we integrate twice we get

uE = (x) = c1x + c2

and applying Boundary condition

uE(x) = T1 + (T2 - T1)x/L.

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